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Method for obtaining powder from highly concentrated high viscous solutions

a high viscosity solution and powder technology, applied in solvent extraction, separation process, filtration separation, etc., can solve the problems of difficult crystallization of sugar mixtures, difficult crystallization of solutions containing oligosaccharaides, and difficult separation of simple separations

Inactive Publication Date: 2004-10-12
OLADUR
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

"The present invention provides an economical method for obtaining purified solid substances from highly concentrated viscous solutions containing solutes and solvents. The method involves subjecting the solution to high shear mixing with a second solvent that is miscible with the first solvent. The second solvent is added while subjecting the solution to high shear mixing, resulting in a suspension of fine particles in a liquid phase consisting of the first and second solvents. The solids can then be easily separated by filtration. This method is simple, does not require complicated equipment, and the solids are obtained as dry, non-sticky pure powder that does not adhere to equipment walls and does not cause clogging problems. The method is particularly useful for de-oiling commercial lecithin powder."

Problems solved by technology

In particular, such difficulties arise when the solids present in the solution constitute a mixture and not a pure substance, as often occurs in the processing of substances from natural sources.
In situations like that, the solute does not crystallize easily, preventing simple separation.
For example, it is well known that solutions of sugar mixtures (i.e., molasses) and especially those which contain oligosaccharaides, are very difficult to crystallize.
Recovery of the solids by means of solvent evaporation also fails many times to give pure and fine solid particles, since small amounts of liquid are entrapped between the amorphous solid skeleton.
Thus, evaporation often results either in a dough-like substance which cannot be dried further or in one lump of hard solid which is difficult to handle and needs to be further pulverized.
Furthermore, soluble contamination remains entrapped in the dried solid so obtained.
Moreover, complete evaporation often requires high temperatures which might destroy the substances to be recovered.
Powders have prolonged shelf life, are easier to handle and to pack and consequently are cheaper to transport, while liquids, having higher volume and weight, impose packaging and leakage problems.
In particular, when relating to food additives, syrup-like additives are limited to "wet-foods" and cannot be used for powdered foodstuff.
However, these methods require sophisticated and expensive equipment, are high energy consuming or need large solvent quantities, and the results are not always satisfactory.
No further purification is achieved by the drying methods and in many cases, the particles formed tend to stick onto the equipment walls and to clog equipment passages, making the process cumbersome and time consuming.
Moreover, in order to spray dry or freeze dry, the concentrated solutions need to be diluted to a much lower concentration, thus these processes are energy consuming as well.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 2

A sample of 47.7. g of commercial lecithin, containing 72.5% acetone insoluble and 1% water, was heated to 70.degree. C. and injected , over a period of 30 seconds, to the inlet of a continuous dispersing instrument (Ultra-Turrax.RTM. basic T-25 equipped with S25 KV-25 F-IL dispersing head and DK 25.11 flow chamber, all manufactured by IKA), through which 104 g of dry acetone (dried over anhydrous sodium sulfate) were circulated in a closed system. The closed system comprised a closed vessel having an inlet and an outlet, connected by tubes to the outlet and inlet, respectively, of the flow chamber. The commercial lecithin was injected to the inline stream of the flow chamber such that it was drawn by the circulating acetone into the flow chamber, thereby the lecithin-acetone mixture was subjected to the high shear mixing at 24,000 rpm, resulting in a suspension of purified lecithin particles which was pumped into the closed vessel. The inlet and outlet of the closed vessel were arr...

example 3

523 g of hot concentrated purified soy molasses containing 79.5% solids was mixed with 5250 g absolute ethanol by means of continuous inline dispersing instrument (Ultra-Turrax.RTM. basic T-25 equipped with S 25 KV-25 F-IL dispersing head and DK 25.11 flow chamber, all manufactured by IKA) operated at 24,000 rpm, as described in Example 2, to obtain a suspension of fine saccharaide particles. The suspension so obtained was filtered through Buchner funnel under vacuum and the precipitate cake was rinsed with 100 g of cold absolute ethanol following by drying under vacuum (0.05 bar) at 58.degree. C. for 5 hours. 366.9 g of stable odorless white powder were obtained. The powder contained 94.8% sugars of the composition given in Table 1.

example 4

184 g of hot purified concentrated soy molasses of 84.9 wt. % solids were added to 1370 g of absolute ethanol under conditions of high shear mixing, as described in Example 1, to obtain a suspension of fine particles. The suspension was filtered by Buchner funnel using filter paper (whatman 42) under vacuum. The precipitate cake was further rinsed by 100 g cold absolute ethanol. The collected precipitate was further dried under vacuum (0.05 bar) at 58.degree. C. for 5 hours, to obtain 139.8 g of odorless white powder containing 90.5% sugars of the composition given in table 2. The soy sugars powder, stored in a closed container, has shown no deterioration signs, nor any changes were observed, for a period of over 12 months.

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Abstract

The present invention relates to a method for obtaining a purified solid powder from highly concentrated, semi-liquid, high viscous solutions containing one or more solutes and a first solvent. The method comprises contacting the highly concentrated solution with a second solvent under high shear mixing, wherein the second solvent is miscible with the first solvent and wherein the solute has very low solubility or no solubility at all in the second solvent. Thereby a suspension of purified fine particles is obtained which can be easily separated to obtain a fine powder of the solute.

Description

1. Field of the InventionThe present invention relates to a method for recovering dry solid powder from highly concentrated, high viscous solutions.2. Discussion of the Related ArtDifficulties in recovering dry solid particles from highly concentrated, high viscous, semi-liquids solutions are known in the art. In particular, such difficulties arise when the solids present in the solution constitute a mixture and not a pure substance, as often occurs in the processing of substances from natural sources. In situations like that, the solute does not crystallize easily, preventing simple separation. For example, it is well known that solutions of sugar mixtures (i.e., molasses) and especially those which contain oligosaccharaides, are very difficult to crystallize. Recovery of the solids by means of solvent evaporation also fails many times to give pure and fine solid particles, since small amounts of liquid are entrapped between the amorphous solid skeleton. Thus, evaporation often res...

Claims

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Application Information

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Patent Type & Authority Patents(United States)
IPC IPC(8): A23J7/00B01D11/04C11B9/02C13J1/00C13J1/02C13B35/02
CPCA23J7/00B01D11/0434C11B9/025C13B35/02B01D11/0492
Inventor CEGLA, URIEL G.SHUSTER, MOSHE
Owner OLADUR